JPS585233B2 - Jiyunkatsuyuso Saibutsu - Google Patents
Jiyunkatsuyuso SaibutsuInfo
- Publication number
- JPS585233B2 JPS585233B2 JP49083759A JP8375974A JPS585233B2 JP S585233 B2 JPS585233 B2 JP S585233B2 JP 49083759 A JP49083759 A JP 49083759A JP 8375974 A JP8375974 A JP 8375974A JP S585233 B2 JPS585233 B2 JP S585233B2
- Authority
- JP
- Japan
- Prior art keywords
- hydrocarbon oil
- oil
- parts
- aromatic hydrocarbon
- properties
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
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- Organic Insulating Materials (AREA)
- Lubricants (AREA)
Description
【発明の詳細な説明】
本発明は潤滑油組成物、詳しくは低温流動性、粘度特性
、電気特性、酸化安定性および熱安定性にすぐれた潤滑
油組成物に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a lubricating oil composition, and more particularly to a lubricating oil composition having excellent low-temperature fluidity, viscosity properties, electrical properties, oxidative stability, and thermal stability.
さらに詳しくは、石油類の熱分解の際に副生ずる高芳香
族炭化水素油の水素化精製物、核水素化物または該水素
化精製物もしくは該核水素化物のアルキル化物より選ば
れる少なくとも1種の炭化水素油と炭素数2〜4のモノ
オレフィンないしはジオレフィンのうちから選ばれる少
なくとも1種の化合物の単独重合体もしくは共重合体か
らなる潤滑油組成物に関する。More specifically, at least one selected from hydrorefined products, nuclear hydrides, and alkylated products of the hydrorefined products or the nuclear hydrides of highly aromatic hydrocarbon oils produced as a by-product during thermal decomposition of petroleum. The present invention relates to a lubricating oil composition comprising a homopolymer or copolymer of a hydrocarbon oil and at least one compound selected from monoolefins and diolefins having 2 to 4 carbon atoms.
一般に石油類を500℃以上の高温で熱分解するとその
残渣油として高芳香族の炭化水素油が副生ずるが、この
高芳香族炭化水素油は色安定性が悪い、熱安定性、酸化
安定性が悪い等の欠点を有している為に有効な利用方法
もなく、工業的にはカーボンブラック、燃料油調合剤な
どに利用されていたにすぎない。Generally, when petroleum is thermally decomposed at a high temperature of 500℃ or higher, highly aromatic hydrocarbon oil is produced as a residual oil, but this highly aromatic hydrocarbon oil has poor color stability, thermal stability, and oxidation stability. Since it has disadvantages such as poor oxidation, there is no effective way to use it, and industrially it has only been used in carbon black, fuel oil preparations, etc.
この高芳香族炭化水素油は芳香族炭化水素として多環芳
香族炭化水素を主として含有しており、近年これを潤滑
油に使用しようとする各種の研究がなされている。This highly aromatic hydrocarbon oil mainly contains polycyclic aromatic hydrocarbons as aromatic hydrocarbons, and in recent years various studies have been conducted to use this as a lubricating oil.
例えば、高芳香族炭化水素油を水素化精製、核水素化あ
るいはアルキル化などの処理を行なうことにより潤滑油
基油の必要条件である低温流動性、電気特性などの諸性
質に対して種々に改良が施されてきた。For example, by subjecting highly aromatic hydrocarbon oil to treatments such as hydrorefining, nuclear hydrogenation, or alkylation, various properties such as low-temperature fluidity and electrical properties, which are necessary conditions for lubricant base oils, can be improved. Improvements have been made.
しかしながら、こうした処理を加えられた炭化水素油に
おいても粘度あるいは粘度指数が低いこと、熱安定性が
低いこと等数多くの欠点を有し、潤滑油基油とするには
十分でなかった。However, even hydrocarbon oils subjected to such treatments have many drawbacks such as low viscosity or viscosity index and low thermal stability, and are not sufficient to be used as lubricating oil base oils.
本発明者らは該高芳香族炭化水素油の各種処理物のもつ
好ましい性状、例えば低温流動性、電気特性などについ
ては何らこれを損なうことなく、粘度、粘度指数および
熱安定性を大幅に向上させる方法を鋭意研究した結果、
平均分子量200〜3000のポリオレフィンを該処理
油に適当量配合することによりこの目的が達成できるこ
とを見出し本発明の完成に至った。The present inventors have found that the viscosity, viscosity index, and thermal stability have been significantly improved without impairing the favorable properties of various processed products of the highly aromatic hydrocarbon oil, such as low-temperature fluidity and electrical properties. As a result of intensive research on how to
It was discovered that this object could be achieved by blending an appropriate amount of polyolefin with an average molecular weight of 200 to 3,000 into the treated oil, and the present invention was completed.
本発明の潤滑油組成物は、
(1) 石油類の500℃以上での熱分解の際に副生
する沸点範囲250〜380℃の高芳香族炭化水素油の
水素化精製物、該炭化水素油の核水素化物もしくは該水
素化精製物ないしは該核水素化物に炭素数1〜6のアル
キル基を少なくとも1個付加させたアルキル化物より選
ばれる少なく1種の炭化水素油55〜95部、
(2)炭素数2〜4のモノオレフィンないしはジオレフ
ィンの中から選ばれる少なくとも1種の化合物を重合し
て得られる単独重合体もしくは共重合体のうち平均分子
量200〜3000のポリオレフィン45〜5部
から成ることを特徴とするものである。The lubricating oil composition of the present invention comprises (1) a hydrorefined product of highly aromatic hydrocarbon oil with a boiling point range of 250 to 380°C, which is produced as a by-product during thermal decomposition of petroleum at 500°C or higher; ( 2) From 45 to 5 parts of a polyolefin with an average molecular weight of 200 to 3000 among homopolymers or copolymers obtained by polymerizing at least one compound selected from monoolefins or diolefins having 2 to 4 carbon atoms. It is characterized by:
本発明の潤滑油組成物の1成分は石油類、例えばナフサ
、灯油、軽油、原油などの500℃以上での熱分解の際
に副生する沸点範囲250〜380℃の高芳香族炭化水
素油を水素化精製することにより得られる芳香族系炭化
水素油、該高芳香族炭化水素油の核水素化物であるとこ
ろのナフテン系炭化水素あるいはナフテン、系炭化水素
油のアルキル化物より成る群より選ばれた少なくとも1
種の炭化水素油である。One component of the lubricating oil composition of the present invention is a highly aromatic hydrocarbon oil with a boiling point range of 250 to 380°C, which is produced as a by-product during thermal decomposition of petroleum, such as naphtha, kerosene, light oil, and crude oil at 500°C or higher. Aromatic hydrocarbon oil obtained by hydrorefining, a naphthenic hydrocarbon which is a nuclear hydride of the highly aromatic hydrocarbon oil, or an alkylated product of a naphthene-based hydrocarbon oil. at least 1
It is a type of hydrocarbon oil.
高芳香族炭化水素油の水素化精製は石油類の通常の水素
化精製法を応用することができる。For the hydrorefining of highly aromatic hydrocarbon oils, ordinary hydrorefining methods for petroleum oils can be applied.
例えば、触媒としてはニッケル、コバルト、モリブデン
、タングステン等の遷移金属又はそれらの酸化物モしく
は硫化物をアルミナ、シリカアルミナなどの担体に担持
させたものを使用することができ、反応剥牛についても
温度250〜400℃、圧力20〜50 kg/cmG
、水素/油モル比2〜10、液空間速度(LH8V)1
〜5等の条件を採用することができる。For example, as a catalyst, transition metals such as nickel, cobalt, molybdenum, and tungsten, or their oxides or sulfides supported on a carrier such as alumina or silica-alumina can be used. Temperature: 250-400℃, pressure: 20-50 kg/cmG
, hydrogen/oil molar ratio 2-10, liquid hourly space velocity (LH8V) 1
Conditions such as ~5 can be adopted.
芳香族炭化水素油の核水素化は、例えば、触媒としては
水素化精製と同じものを使用し、温度100〜300℃
、圧力常圧300kg/cm’G、水素/油モル比5〜
20、LH8VO15〜2.0等の通常の核水素化条件
下で行なうことができる。For nuclear hydrogenation of aromatic hydrocarbon oil, for example, the same catalyst used for hydrorefining is used, and the temperature is 100 to 300°C.
, normal pressure 300 kg/cm'G, hydrogen/oil molar ratio 5~
It can be carried out under normal nuclear hydrogenation conditions such as 20, LH8VO15-2.0.
芳香族系炭化水素油およびナフテン系炭化水素油のアル
キル化物を得るためには各種のアルキル化剤によるアル
キル化反応を適用することができる。In order to obtain alkylated products of aromatic hydrocarbon oils and naphthenic hydrocarbon oils, alkylation reactions using various alkylating agents can be applied.
このアルキル化反応はオレフィン、アルコールなどをア
ルキル化剤とし、シリカアルミナ、リン酸−ケイソウ土
、ゼオライト、活性白土、酸性白土などの固体酸触媒、
あるいは無水塩化アルミニウム、塩化亜鉛などのハロゲ
ン化物、あるいはリン酸、硫酸、沸化水素酸なとの鉱酸
類を用い、各触媒に適した通常の反応条件で行なうこと
ができる。This alkylation reaction uses an olefin, alcohol, etc. as an alkylating agent, a solid acid catalyst such as silica alumina, phosphoric acid-diatomaceous earth, zeolite, activated clay, acid clay, etc.
Alternatively, the reaction can be carried out using halides such as anhydrous aluminum chloride and zinc chloride, or mineral acids such as phosphoric acid, sulfuric acid, and hydrofluoric acid, under usual reaction conditions suitable for each catalyst.
本発明の潤滑油組成物の1つの成分である平均分子量2
00〜3000、好ましくは平均分子量250〜250
0のポリオレフィンは炭素数2〜4のモノオレフィンな
いしはジオレフィンを原料とし、塩化アルミニウム、塩
化マグネシウム、沸化ホウ素、四塩化チタンなどのいわ
ゆるフリーデル・クラフッ型触媒またはそれらの錯化合
物などを触媒とし、必要に応じて有機ハライドや塩酸な
どの助触媒を用い、−30〜30℃で重合させることに
より得ることができる。Average molecular weight 2, which is one component of the lubricating oil composition of the present invention
00-3000, preferably average molecular weight 250-250
0 polyolefin is made from a monoolefin or diolefin having 2 to 4 carbon atoms, and uses a so-called Friedel-Krach type catalyst such as aluminum chloride, magnesium chloride, boron fluoride, titanium tetrachloride, or a complex compound thereof as a catalyst. It can be obtained by polymerizing at -30 to 30°C, using a promoter such as an organic halide or hydrochloric acid as necessary.
これらポリオレフィンのうちポリブテンが最も好ましい
。Among these polyolefins, polybutene is most preferred.
ポリオレフィンのうち平均分子量が200より小さいも
のは引火点が低すぎ安全性に問題があり、また平均分子
量が3000より太きいものは粘度が高すぎること、低
温流動性、粘度特性が良くないこと、および芳香族系炭
化水素油、ナフテン系炭化水素油あるいはこれらのアル
キル化物に対する溶解性が良くないことなどの理由で好
ましくない。Among polyolefins, polyolefins with an average molecular weight smaller than 200 have a safety problem because their flash point is too low, and polyolefins with an average molecular weight larger than 3000 have too high a viscosity and poor low-temperature fluidity and viscosity properties. Also, they are not preferred because they have poor solubility in aromatic hydrocarbon oils, naphthenic hydrocarbon oils, or alkylated products thereof.
本発明の潤滑油組成物は低温流動性、電気特性などの好
ましい性状に加え、粘度、粘度指数、熱安定性などの点
で優れた性状を有するため、潤滑油特に絶縁油、冷凍機
油、作動油など苛酷な条件下で使用される潤滑油に適す
る。The lubricating oil composition of the present invention has excellent properties such as viscosity, viscosity index, and thermal stability in addition to favorable properties such as low-temperature fluidity and electrical properties. Suitable for lubricating oils used under harsh conditions such as oil.
例えば、本発明の潤滑油組成物を冷凍機油として用いた
場合、吐出弁などの高温部にスラッジの発生が少ないこ
と、冷媒に対する安定性が良いこと等従来の潤滑油には
見られなかった諸性質が得られる。For example, when the lubricating oil composition of the present invention is used as a refrigerating machine oil, it has various properties not found in conventional lubricating oils, such as less sludge generation in high-temperature parts such as discharge valves, and good stability against refrigerants. properties are obtained.
本発明において所望ならば潤滑油の用途に応じて上記組
成物に、粘度指数向上剤、酸化防止剤、清浄分散剤、金
属不活性化剤、消泡剤、流動点降下剤をはじめとする各
種の添加剤を加えることができる。In the present invention, if desired, various additives such as viscosity index improvers, antioxidants, detergent dispersants, metal deactivators, antifoaming agents, pour point depressants, etc. may be added to the above composition depending on the use of the lubricating oil. Additives can be added.
その数例を挙げると粘度指数向上剤としては、例えばポ
リアクリレート、ポリメタアクリレート、ポリイソブチ
レン、エチレンプロピレンコポリマー、酸化防止剤とし
ては、例えばジアルキルジチオリン酸金属塩、フェニル
−α−ナフチルアミン、2・6−ジーt−ブチルパラク
レゾール、2・6−ジーt−ブチルフェノール、清浄分
散剤としては、例えば金属スルフォネートあるいは金属
フオスフオネートなどの中性塩、塩基性塩、超塩基性塩
又はアルケニルコハク酸イミド、ベンジルアミン類など
の無灰型分散剤、金属不活性化剤としては、例えばベン
ゾトリアゾール、消泡剤としては例えばシリコーン類、
低分子量ポリメタクリレートなどがある。To name a few, viscosity index improvers include polyacrylate, polymethacrylate, polyisobutylene, ethylene propylene copolymer, and antioxidants include dialkyldithiophosphate metal salts, phenyl-α-naphthylamine, 2.6 - di-t-butyl para-cresol, 2,6-di-t-butylphenol, as detergents and dispersants, for example neutral salts, basic salts, ultrabasic salts such as metal sulfonates or metal phosphonates or alkenylsuccinimides, benzyl Ashless dispersants such as amines, metal deactivators include benzotriazole, antifoaming agents include silicones,
Examples include low molecular weight polymethacrylates.
これらの各種添加剤は1種もしくは2種以上の混合系で
使用することができ、潤滑油組成物全量に対し0.1〜
10,0重量%添加することができる。These various additives can be used alone or in a mixed system of two or more, and are added in amounts of 0.1 to 0.1 to the total amount of the lubricating oil composition.
It can be added in an amount of 10.0% by weight.
以下本発明をより具体的に説明するために、実施例を挙
げる。Examples will be given below to more specifically explain the present invention.
実施例 1
芳香族系炭化水素油性(1) 60〜90部ポ
リブデン注(2) 40〜10部注
(1)ナフサの熱分解により得られる沸点300〜37
0℃の高芳香族留分を水素
化精製したもの。Example 1 Aromatic hydrocarbon oil (1) 60 to 90 parts Polybutene Note (2) 40 to 10 parts Note (1) Boiling point obtained by thermal decomposition of naphtha 300 to 37
Hydrorefined highly aromatic fraction at 0°C.
処理条件は以下のとおりである。The processing conditions are as follows.
注(2)ナフサ分解により生成するブタン−ブテン留分
のうち、イソブチレンを主体と
し、1部n−ブテンを含有するものを塩
化アルミニウム触媒により重合させた共
重合物質で平均分子量350、粘度が
29 cst (100下)及び4.5(2101)の
もの。Note (2) Among the butane-butene fractions produced by naphtha decomposition, it is a copolymerized material that is mainly composed of isobutylene and contains a portion of n-butene using an aluminum chloride catalyst, and has an average molecular weight of 350 and a viscosity of 29. cst (below 100) and 4.5 (2101).
実施例1の組成物について電気絶縁油としての性状を測
定した結果を以下に示す。The results of measuring the properties of the composition of Example 1 as an electrical insulating oil are shown below.
いずれも低温流動性、電気特性、耐熱安定性に優れた組
成物であった。All of the compositions were excellent in low-temperature fluidity, electrical properties, and heat-resistant stability.
実施例 2
注(1)
芳香族系炭化水素油アルキル化物 70部ポリブ
テン注(2) 30部注1
)実施例1の芳香族系炭化水素油のうち沸点250〜3
00℃のものをエチレン
によりアルキル化したもので沸点270
〜370℃のもの。Example 2 Note (1) Aromatic hydrocarbon oil alkylated product 70 parts Polybutene Note (2) 30 parts Note 1
) Aromatic hydrocarbon oil of Example 1 with a boiling point of 250 to 3
00°C, alkylated with ethylene and has a boiling point of 270 to 370°C.
アルキル化条件は以下のとおりである。The alkylation conditions are as follows.
実施例2の組成物について耐熱冷凍機油としての性状を
測定した結果を以下に示す。The results of measuring the properties of the composition of Example 2 as a heat-resistant refrigerating machine oil are shown below.
本実施例組成物はJIS K2211冷凍機油規格を
満たし、特に冷媒に対する安定度、低温流動性にすぐれ
、従来のものに対しはるかに長時間の使用に耐えた。The composition of this example met the JIS K2211 refrigerating machine oil standard, was particularly excellent in stability against refrigerants and low-temperature fluidity, and could withstand use for a much longer time than conventional compositions.
実施例 3
ナフテン系炭化水素油性(1) 70部ポリ
ブチ、注(2) 3o部注(1
) ナフサの熱分解により得られる沸点210〜37
0℃の高芳香族留分を水素
化精製し、さらに核水素化したもので、
沸点が265〜307℃のもの。Example 3 Naphthenic hydrocarbon oil (1) 70 parts polybutylene, Note (2) 3o parts Note (1)
) Boiling point 210-37 obtained by thermal decomposition of naphtha
A highly aromatic fraction at 0°C is hydrorefined and then subjected to nuclear hydrogenation, with a boiling point of 265 to 307°C.
処理条件は以下の通りである。The processing conditions are as follows.
実施例4の組成物について作動油としての性状を測定し
た結果を以下に示す。The results of measuring the properties of the composition of Example 4 as a hydraulic oil are shown below.
Claims (1)
点範囲250〜380℃の高芳香族炭化水素油の水素化
精製物、該炭化水素油の核水素化物もしくは該水素化精
製物ないしは該核水素化物に炭素数1〜6のアルキル基
を少なくとも1個付加させたアルキル化物より選ばれる
少なくとも1種の炭化水素油55〜95部と炭素数2〜
4のモノオレフィンないしはジオレフィンの中から選ば
れる少なくとも1種の化合物を重合して得られる単独重
合体もしくは共重合体のうち平均分子量200〜300
0のポリオレフィン45〜5部から成ることを特徴とす
る潤滑油組成物。1 A hydrorefined product of highly aromatic hydrocarbon oil with a boiling point range of 250 to 380°C, a nuclear hydride of the hydrocarbon oil, or a hydrorefined product of the hydrocarbon oil, which is a by-product during thermal decomposition of petroleum at 500°C or higher. or 55 to 95 parts of at least one hydrocarbon oil selected from alkylated products obtained by adding at least one alkyl group having 1 to 6 carbon atoms to the nuclear hydride, and 55 to 95 parts of at least one hydrocarbon oil having 2 to 6 carbon atoms.
A homopolymer or copolymer obtained by polymerizing at least one compound selected from the monoolefins or diolefins of No. 4 with an average molecular weight of 200 to 300.
A lubricating oil composition characterized in that it consists of 45 to 5 parts of a polyolefin of 0.0 to 5.0 parts.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP49083759A JPS585233B2 (en) | 1974-07-23 | 1974-07-23 | Jiyunkatsuyuso Saibutsu |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP49083759A JPS585233B2 (en) | 1974-07-23 | 1974-07-23 | Jiyunkatsuyuso Saibutsu |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5112802A JPS5112802A (en) | 1976-01-31 |
| JPS585233B2 true JPS585233B2 (en) | 1983-01-29 |
Family
ID=13811480
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP49083759A Expired JPS585233B2 (en) | 1974-07-23 | 1974-07-23 | Jiyunkatsuyuso Saibutsu |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS585233B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0236716A (en) * | 1988-07-25 | 1990-02-06 | Nippon Telegr & Teleph Corp <Ntt> | Circuitbreaker for floor wiring and floor wiring method |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9637424B1 (en) | 2014-12-16 | 2017-05-02 | Exxonmobil Research And Engineering Company | High octane gasoline and process for making same |
| US9637423B1 (en) | 2014-12-16 | 2017-05-02 | Exxonmobil Research And Engineering Company | Integrated process for making high-octane gasoline |
| CN107001949A (en) | 2014-12-16 | 2017-08-01 | 埃克森美孚研究工程公司 | Paraffin upgrading to produce distillate oil and lubricant base oil |
| US10023533B2 (en) | 2014-12-16 | 2018-07-17 | Exxonmobil Research And Engineering Company | Process to produce paraffinic hydrocarbon fluids from light paraffins |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS513322B2 (en) * | 1971-12-13 | 1976-02-02 | ||
| BE781636A (en) * | 1972-04-04 | 1972-07-31 | Labofina Sa | LUBRICATING COMPOSITIONS FOR TWO STROKE ENGINES. |
| JPS5514231B2 (en) * | 1972-05-19 | 1980-04-15 | ||
| US3808134A (en) * | 1972-08-09 | 1974-04-30 | Continental Oil Co | Synthetic hydrocarbon lubricant compositions |
| US3812036A (en) * | 1972-10-02 | 1974-05-21 | Continental Oil Co | Preparation of synthetic hydrocarbon lubrication |
-
1974
- 1974-07-23 JP JP49083759A patent/JPS585233B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0236716A (en) * | 1988-07-25 | 1990-02-06 | Nippon Telegr & Teleph Corp <Ntt> | Circuitbreaker for floor wiring and floor wiring method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5112802A (en) | 1976-01-31 |
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